Thermal energy storage system coupled with steam cracking system
An energy storage system (TES) converts variable renewable electricity (VRE) to continuous heat at over 1000° C. Intermittent electrical energy heats a solid medium. Heat from the solid medium is delivered continuously on demand. Heat delivery via flowing gas establishes a thermocline which maintains high outlet temperature throughout discharge. The delivered heat which may be used for processes including power generation and cogeneration. In one application, the energy storage system provides higher-temperature heat to a steam cracking furnace system for converting a hydrocarbon feedstock into cracked gas, thereby increasing the efficiency of the temperature control.
1. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, comprising:
a preheating section configured to preheat a hydrocarbon feedstock, and to mix the preheated hydrocarbon feedstock with dilution steam to produce a preheated mixture of the hydrocarbon feedstock and the dilution steam;
an electric cracker configured to convert the preheated mixture into a cracked gas at high temperature;
a thermal energy storage (TES) system configured to store thermal energy derived from electricity generated by an energy source and converting the electricity into heat for storage in a thermal energy storage medium and providing the stored heat to the preheating section;
a cooling section including at least one quench exchanger configured to quench the cracked gas; and
an export steam generation subsystem, wherein the steam cracking system is configured to provide heat to the export steam generation subsystem from both the cooling section and from the TES system.
2. The steam cracking system of claim 1 , further including a thermal power cycle subsystem configured to receive steam from the export steam generation subsystem and to generate electricity to be provided to the electric cracker.
3. The steam cracking system of claim 1 , wherein the energy source is a variable renewable energy source having intermittent availability.
4. The steam cracking system of claim 1 , further including a convection section and an electric booster heater configured to increase the temperature of a heated fluid prior to reaching the convection section.
5. The steam cracking system of claim 1 , further including a convection section configured to exhaust heated fluid and direct the exhausted heated fluid back as an input to the TES system for reheating.
6. The steam cracking system of claim 5 , further configured to cool the heated fluid to remove water vapor via condensation prior to input to the TES system.
7. The steam cracking system of claim 1 , further including a first heat exchanger configured to preheat the hydrocarbon feedstock using a heated fluid provided by the TES system.
8. The steam cracking system of claim 1 , further including a heat exchanger configured to produce superheated dilution steam heated in a conventional steam-cracking process using heated fluid provided by the TES system.
9. The steam cracking system of claim 1 , wherein the thermal energy storage medium includes refractory material.
10. The steam cracking system of claim 8 , wherein the heat exchanger is further configured to produce other material streams heated in the conventional steam-cracking process using the heated fluid provided by the TES system.
11. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, comprising:
a preheating section configured to preheat a hydrocarbon feedstock, and to mix the preheated hydrocarbon feedstock with dilution steam to produce a preheated mixture of the hydrocarbon feedstock and the dilution steam;
an electric cracker configured to convert the preheated mixture into a cracked gas at high temperature;
a thermal energy storage (TES) system configured to store thermal energy derived from electricity generated by an energy source and converting the electricity into heat for storage in a thermal energy storage medium and providing the stored heat to the preheating section; and
an export steam generation subsystem, wherein the steam cracking system is configured to provide heat to the export steam generation subsystem from the TES system.
12. The steam cracking system of claim 11 , further including a cooling section including at least one quench exchanger configured to quench the cracked gas.
13. The steam cracking system of claim 12 , further configured to provide heat to the export steam generation subsystem from the cooling section.
14. The steam cracking system of claim 13 , further including a thermal power cycle subsystem configured to receive steam from the export steam generation subsystem and to generate electricity to be provided to the electric cracker.
15. The steam cracking system of claim 11 , further including a thermal power cycle subsystem configured to receive steam from the export steam generation subsystem and to generate electricity to be provided to the electric cracker.
16. The steam cracking system of claim 11 , wherein the energy source is a variable renewable energy source having intermittent availability.
17. The steam cracking system of claim 11 , further including a convection section and an electric booster heater configured to increase the temperature of a heated fluid prior to reaching the convection section.
18. The steam cracking system of claim 11 , further including a convection section configured to exhaust heated fluid and direct the exhausted heated fluid back as an input to the TES system for reheating.
19. The steam cracking system of claim 18 , further configured to cool the heated fluid to remove water vapor via condensation prior to input to the TES system.
20. The steam cracking system of claim 11 , further including a first heat exchanger configured to preheat the hydrocarbon feedstock using a heated fluid provided by the TES system.
21. The steam cracking system of claim 11 , further including a heat exchanger configured to produce superheated dilution steam heated in a conventional steam-cracking process using heated fluid provided by the TES system.
22. The steam cracking system of claim 11 , wherein the thermal energy storage medium includes refractory material.
23. The steam cracking system of claim 21 , wherein the heat exchanger is further configured to produce other material streams heated in the conventional steam-cracking process using the heated fluid provided by the TES system.
24. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, comprising:
a preheating section configured to preheat a hydrocarbon feedstock, and to mix the preheated hydrocarbon feedstock with dilution steam to produce a preheated mixture of the hydrocarbon feedstock and the dilution steam;
an electric cracker configured to convert the preheated mixture into a cracked gas at high temperature;
a thermal energy storage (TES) system configured to store thermal energy derived from electricity generated by an energy source and converting the electricity into heat for storage in a thermal energy storage medium and providing the stored heat to the preheating section;
a convection section; and
an electric booster heater configured to increase the temperature of a heated fluid prior to reaching the convection section.
25. The steam cracking system of claim 22 , further including a cooling section including at least one quench exchanger configured to quench the cracked gas.
26. The steam cracking system of claim 25 , further including:
an export steam generation subsystem, wherein the steam cracking system is configured to provide heat to the export steam generation subsystem from both the cooling section and from the TES system.
27. The steam cracking system of claim 26 , further including a thermal power cycle subsystem configured to receive steam from an export steam generation subsystem and to generate electricity to be provided to the electric cracker.
28. The steam cracking system of claim 24 , wherein the energy source is a variable renewable energy source having intermittent availability.
29. The steam cracking system of claim 24 , wherein the convection section is configured to exhaust heated fluid and direct the exhausted heated fluid back as an input to the TES system for reheating.
30. The steam cracking system of claim 29 , further configured to cool the heated fluid to remove water vapor via condensation prior to input to the TES system.
31. The steam cracking system of claim 24 , further including a first heat exchanger configured to preheat the hydrocarbon feedstock using a heated fluid provided by the TES system.
32. The steam cracking system of claim 24 , further including a heat exchanger configured to produce superheated dilution steam heated in a conventional steam-cracking process using heated fluid provided by the TES system.
33. The steam cracking system of claim 24 , wherein the thermal energy storage medium includes refractory material.
34. The steam cracking system of claim 32 , wherein the heat exchanger is further configured to produce other material streams heated in the conventional steam-cracking process using the heated fluid provided by the TES system.
35. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, comprising:
a preheating section configured to preheat a hydrocarbon feedstock, and to mix the preheated hydrocarbon feedstock with dilution steam to produce a preheated mixture of the hydrocarbon feedstock and the dilution steam;
an electric cracker configured to convert the preheated mixture into a cracked gas at high temperature;
a thermal energy storage (TES) system configured to store thermal energy derived from electricity generated by an energy source and converting the electricity into heat for storage in a thermal energy storage medium and providing the stored heat to the preheating section; and
a convection section configured to exhaust heated fluid and direct the exhausted heated fluid back as an input to the TES system for reheating.
36. The steam cracking system of claim 35 , further including a cooling section including at least one quench exchanger configured to quench the cracked gas.
37. The steam cracking system of claim 36 , further including an export steam generation subsystem, wherein the steam cracking system is configured to provide heat to the export steam generation subsystem from both the cooling section and from the TES system.
38. The steam cracking system of claim 37 , further including a thermal power cycle subsystem configured to receive steam from the export steam generation subsystem and to generate electricity to be provided to the electric cracker.
39. The steam cracking system of claim 35 , wherein the energy source is a variable renewable energy source having intermittent availability.
40. The steam cracking system of claim 35 , further configured to cool the heated fluid to remove water vapor via condensation prior to input to the TES system.
41. The steam cracking system of claim 35 , further including a first heat exchanger configured to preheat the hydrocarbon feedstock using a heated fluid provided by the TES system.
42. The steam cracking system of claim 35 , further including a heat exchanger configured to produce superheated dilution steam heated in a conventional steam-cracking process using heated fluid provided by the TES system.
43. The steam cracking system of claim 33 , wherein the thermal energy storage medium includes refractory material.
44. The steam cracking system of claim 42 , wherein the heat exchanger is further configured to produce other material streams heated in the conventional steam-cracking process using the heated fluid provided by the TES system.
45. A steam cracking system for converting a hydrocarbon feedstock into cracked gas, comprising:
a preheating section configured to preheat a hydrocarbon feedstock, and to mix the preheated hydrocarbon feedstock with dilution steam to produce a preheated mixture of the hydrocarbon feedstock and the dilution steam;
an electric cracker configured to convert the preheated mixture into a cracked gas at high temperature;
a thermal energy storage (TES) system configured to store thermal energy derived from electricity generated by an energy source and converting the electricity into heat for storage in a thermal energy storage medium and providing the stored heat to the preheating section; and
a heat exchanger configured to produce superheated dilution steam heated in a conventional steam-cracking process using heated fluid provided by the TES system.
46. The steam cracking system of claim 43 , further including a cooling section including at least one quench exchanger configured to quench the cracked gas.
47. The steam cracking system of claim 46 , further including:
an export steam generation subsystem, wherein the steam cracking system is configured to provide heat to the export steam generation subsystem from both the cooling section and from the TES system.
48. The steam cracking system of claim 47 , further including a thermal power cycle subsystem configured to receive steam from the export steam generation subsystem and to generate electricity to be provided to the electric cracker.
49. The steam cracking system of claim 43 , wherein the energy source is a variable renewable energy source having intermittent availability.
50. The steam cracking system of claim 43 , further including a first heat exchanger configured to preheat the hydrocarbon feedstock using the heated fluid provided by the TES system.
51. The steam cracking system of claim 43 , wherein the thermal energy storage medium includes refractory material.
52. The steam cracking system of claim 50 , wherein the heat exchanger is further configured to produce other material streams heated in the conventional steam-cracking process using the heated fluid provided by the TES system.